期刊文献+

给水超滤膜系统中曝气对膜通量的影响及其机理研究 被引量:2

Study on mechanisms and impacts of aeration on the membrane flux in drinking water ultrafiltration membrane treatment
下载PDF
导出
摘要 通过系列试验探讨了淹没式给水超滤膜系统中曝气对膜通量的影响及其机理,结果表明:淹没式给水超滤膜系统中膜通量随时间和过滤水量的变化均由快、慢两个指数衰减模式共同组成,其衰减过程符合相似的衰减方程式;曝气可有效改变膜表面的流体流态,提高膜通量,最大假想稳定态膜通量及其最小衰减系数均在曝气条件下达到;曝气强度对膜通量改善影响明显,曝气强度越大,膜通量改善程度越强,但超过一定曝气强度后曝气强度对膜通量改善的影响甚微。 This paper studied the influence of aeration in the submerged drinking water ultrafihration membrane system on membrane flux and its mechanisms. The results showed that: the variance of the membrane flux in the submerged drinking water ultrafiltration membrane system depending on time and permeated flux was composed of rapid and slow exponential evanescent modes, and the evanescent processes matched the similar evanescent equation; aeration could efficiently improve the fluid flow pattern on the membrane surface, increase membrane flux, and realize the maximum theoretical stable membrane flux and the minimum evanescent coefficient; the influence of aeration on mem- brane flux was obvious, the more aeration intensity the better improvement on membrane flux, but the influence became indifferent when the aeration intensity was above certain.
作者 雷晓玲
机构地区 重庆交通大学
出处 《给水排水》 CSCD 北大核心 2009年第11期129-135,共7页 Water & Wastewater Engineering
基金 国家人力资源和社会保障部:2008年度留学人员科技活动择优资助项目(渝人办[2009]11号) Natural Sciences and Engineering Research Council of Canada(NSERC) 重庆交通大学高层次人才科研启动经费项目(交大科[2009]4号)
关键词 给水超滤膜系统 曝气 膜通量 衰减模式 影响机理 Drinking water ultrafiltration system Aeration Membrane flux Evanescent mode Impacts mechanisms
  • 相关文献

参考文献13

  • 1EPA 815 - D- 03 - 008 Membrane filtration guidance manual, 2003.
  • 2Cheng T W. Influent of inclunation on gas-sparged cross-flow ultraflltration through an inorganic tubular membrane. J Membr Sci, 2002,196 (1): 103.
  • 3Cui Z F, Ghosh R, Yu J, et al. An experimental study of flux enhancement with air sparging in a horizontal tubular membrane module. In: Proeeedings of the Sixth World Congress on Chemical Engineering, Melbourne, 2001.
  • 4VerberkJ Q J C, Hoogeveen P E, Futselaar H, et al. Hydraulic distribution of water and air over a membrane module using airflush. Wat Sci and Tech, Water Supply, 2002,2 (2) : 297.
  • 5Cui Z F, Chang S, Fane A G. The use of gas bubbling to enhance membrane processes. J Membr Sci, 2003, (221) : 1.
  • 6Bellara S R, Cui Z F, Pepper D S. Gas sparging to enhance permeate flux in ultrafiltration using hollow fibre membranes. J Membr Sci, 1996,121: 175.
  • 7Ducom G, Puech F P, Cabassud F P. Air sparging with flat sheet nanofiltration: A link between wall shear stress and flux enhancement. Desalination, 2002,145 : 97.
  • 8Cabassud C, Laborie S, Durand-Bourlier I., et al. Air sparging in ultrafiltration hollow fibers: Rdationship between flux enhancement, cake characteristics and hydrodynamic parameters. J Membr Sci,2001, 181(1): 57.
  • 9Taha T,Cui Z F. CFD modelling of gas sparged ultrafiltration in tubular membranes. J Membr Sci, 2002, 210:13.
  • 10Um M J, Yoon S H, Lee C H, et al. Flux enhancement with gas injection in crossflow ultrafiltration of oily wastewater. Pergamon, 2001, (01)00155 - 5.

同被引文献17

引证文献2

二级引证文献8

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部